RU2319684C9 - Способ непрерывного разделения c4-фракции - Google Patents
Способ непрерывного разделения c4-фракции Download PDFInfo
- Publication number
- RU2319684C9 RU2319684C9 RU2005105045/04A RU2005105045A RU2319684C9 RU 2319684 C9 RU2319684 C9 RU 2319684C9 RU 2005105045/04 A RU2005105045/04 A RU 2005105045/04A RU 2005105045 A RU2005105045 A RU 2005105045A RU 2319684 C9 RU2319684 C9 RU 2319684C9
- Authority
- RU
- Russia
- Prior art keywords
- stream
- butenes
- distillation column
- butene
- extractive distillation
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 52
- 238000000895 extractive distillation Methods 0.000 claims abstract description 90
- 239000002904 solvent Substances 0.000 claims abstract description 56
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical class CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims abstract description 52
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 claims abstract description 51
- 235000013844 butane Nutrition 0.000 claims abstract description 46
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 45
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 41
- 238000000926 separation method Methods 0.000 claims abstract description 28
- 239000000126 substance Substances 0.000 claims abstract 2
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 claims description 104
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 claims description 60
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 claims description 58
- 238000004821 distillation Methods 0.000 claims description 39
- IAQRGUVFOMOMEM-UHFFFAOYSA-N but-2-ene Chemical class CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 claims description 35
- 238000009835 boiling Methods 0.000 claims description 20
- 238000000066 reactive distillation Methods 0.000 claims description 16
- 150000001875 compounds Chemical class 0.000 claims description 14
- 125000002534 ethynyl group Chemical class [H]C#C* 0.000 claims description 14
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 13
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims description 12
- 238000005984 hydrogenation reaction Methods 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- MWWATHDPGQKSAR-UHFFFAOYSA-N propyne Chemical compound CC#C MWWATHDPGQKSAR-UHFFFAOYSA-N 0.000 claims description 11
- QNRMTGGDHLBXQZ-UHFFFAOYSA-N buta-1,2-diene Chemical compound CC=C=C QNRMTGGDHLBXQZ-UHFFFAOYSA-N 0.000 claims description 10
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 claims description 10
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 9
- 238000006317 isomerization reaction Methods 0.000 claims description 8
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 claims description 6
- 238000005336 cracking Methods 0.000 claims description 5
- 239000001282 iso-butane Substances 0.000 claims description 5
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 4
- 238000000354 decomposition reaction Methods 0.000 claims description 4
- 230000002269 spontaneous effect Effects 0.000 claims description 4
- 238000006356 dehydrogenation reaction Methods 0.000 claims description 3
- 238000004508 fractional distillation Methods 0.000 claims description 3
- 239000007864 aqueous solution Substances 0.000 claims description 2
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- 238000006471 dimerization reaction Methods 0.000 claims 1
- XNMQEEKYCVKGBD-UHFFFAOYSA-N dimethylacetylene Natural products CC#CC XNMQEEKYCVKGBD-UHFFFAOYSA-N 0.000 claims 1
- 230000004888 barrier function Effects 0.000 abstract 1
- 239000000203 mixture Substances 0.000 description 24
- 239000007788 liquid Substances 0.000 description 8
- WFYPICNXBKQZGB-UHFFFAOYSA-N butenyne Chemical group C=CC#C WFYPICNXBKQZGB-UHFFFAOYSA-N 0.000 description 7
- -1 butines Chemical class 0.000 description 6
- IAQRGUVFOMOMEM-ARJAWSKDSA-N cis-but-2-ene Chemical compound C\C=C/C IAQRGUVFOMOMEM-ARJAWSKDSA-N 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 5
- KDKYADYSIPSCCQ-UHFFFAOYSA-N but-1-yne Chemical group CCC#C KDKYADYSIPSCCQ-UHFFFAOYSA-N 0.000 description 4
- 235000013847 iso-butane Nutrition 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 3
- 238000003795 desorption Methods 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- BKOOMYPCSUNDGP-UHFFFAOYSA-N 2-methylbut-2-ene Chemical compound CC=C(C)C BKOOMYPCSUNDGP-UHFFFAOYSA-N 0.000 description 2
- YEJRWHAVMIAJKC-UHFFFAOYSA-N 4-Butyrolactone Chemical compound O=C1CCCO1 YEJRWHAVMIAJKC-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- BZLVMXJERCGZMT-UHFFFAOYSA-N Methyl tert-butyl ether Chemical compound COC(C)(C)C BZLVMXJERCGZMT-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 125000001931 aliphatic group Chemical group 0.000 description 2
- IYABWNGZIDDRAK-UHFFFAOYSA-N allene Chemical compound C=C=C IYABWNGZIDDRAK-UHFFFAOYSA-N 0.000 description 2
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 2
- 150000001408 amides Chemical class 0.000 description 2
- 239000001273 butane Substances 0.000 description 2
- 238000004523 catalytic cracking Methods 0.000 description 2
- 150000003950 cyclic amides Chemical class 0.000 description 2
- 210000000540 fraction c Anatomy 0.000 description 2
- 239000002638 heterogeneous catalyst Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 2
- 238000004230 steam cracking Methods 0.000 description 2
- NUMQCACRALPSHD-UHFFFAOYSA-N tert-butyl ethyl ether Chemical compound CCOC(C)(C)C NUMQCACRALPSHD-UHFFFAOYSA-N 0.000 description 2
- 238000004227 thermal cracking Methods 0.000 description 2
- IAQRGUVFOMOMEM-ONEGZZNKSA-N trans-but-2-ene Chemical compound C\C=C\C IAQRGUVFOMOMEM-ONEGZZNKSA-N 0.000 description 2
- DURPTKYDGMDSBL-UHFFFAOYSA-N 1-butoxybutane Chemical compound CCCCOCCCC DURPTKYDGMDSBL-UHFFFAOYSA-N 0.000 description 1
- SFPQDYSOPQHZAQ-UHFFFAOYSA-N 2-methoxypropanenitrile Chemical compound COC(C)C#N SFPQDYSOPQHZAQ-UHFFFAOYSA-N 0.000 description 1
- UPOMCDPCTBJJDA-UHFFFAOYSA-N 2-methyl-1-[(2-methylpropan-2-yl)oxy]propane Chemical compound CC(C)COC(C)(C)C UPOMCDPCTBJJDA-UHFFFAOYSA-N 0.000 description 1
- FITVQUMLGWRKKG-UHFFFAOYSA-N 2-methyl-2-propoxypropane Chemical compound CCCOC(C)(C)C FITVQUMLGWRKKG-UHFFFAOYSA-N 0.000 description 1
- YHQXBTXEYZIYOV-UHFFFAOYSA-N 3-methylbut-1-ene Chemical compound CC(C)C=C YHQXBTXEYZIYOV-UHFFFAOYSA-N 0.000 description 1
- WPSLQNRZBTVEJC-UHFFFAOYSA-N C(=O)N1CCOCC1.CC(=O)N(C)C Chemical compound C(=O)N1CCOCC1.CC(=O)N(C)C WPSLQNRZBTVEJC-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 241000482967 Diloba caeruleocephala Species 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 1
- SUAKHGWARZSWIH-UHFFFAOYSA-N N,N‐diethylformamide Chemical compound CCN(CC)C=O SUAKHGWARZSWIH-UHFFFAOYSA-N 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 239000000010 aprotic solvent Substances 0.000 description 1
- HHEMIMSLFVBJMH-UHFFFAOYSA-N but-1-yne Chemical compound C#CCC.C(C)C#C HHEMIMSLFVBJMH-UHFFFAOYSA-N 0.000 description 1
- 229930188620 butyrolactone Natural products 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 238000011437 continuous method Methods 0.000 description 1
- 239000006184 cosolvent Substances 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- AQEFLFZSWDEAIP-UHFFFAOYSA-N di-tert-butyl ether Chemical class CC(C)(C)OC(C)(C)C AQEFLFZSWDEAIP-UHFFFAOYSA-N 0.000 description 1
- 150000001993 dienes Chemical class 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 150000003951 lactams Chemical class 0.000 description 1
- 239000003915 liquefied petroleum gas Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 230000009972 noncorrosive effect Effects 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000000546 pharmaceutical excipient Substances 0.000 description 1
- FVSKHRXBFJPNKK-UHFFFAOYSA-N propionitrile Chemical compound CCC#N FVSKHRXBFJPNKK-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000001577 simple distillation Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/04—Purification; Separation; Use of additives by distillation
- C07C7/05—Purification; Separation; Use of additives by distillation with the aid of auxiliary compounds
- C07C7/08—Purification; Separation; Use of additives by distillation with the aid of auxiliary compounds by extractive distillation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/141—Fractional distillation or use of a fractionation or rectification column where at least one distillation column contains at least one dividing wall
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
- B01D3/40—Extractive distillation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Water Supply & Treatment (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10233620.2 | 2002-07-24 | ||
DE10233620A DE10233620A1 (de) | 2002-07-24 | 2002-07-24 | Kontinuierliches Verfahren zur Auftrennung eines C4-Schnittes |
Publications (3)
Publication Number | Publication Date |
---|---|
RU2005105045A RU2005105045A (ru) | 2005-07-20 |
RU2319684C2 RU2319684C2 (ru) | 2008-03-20 |
RU2319684C9 true RU2319684C9 (ru) | 2008-08-20 |
Family
ID=30128331
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU2005105045/04A RU2319684C9 (ru) | 2002-07-24 | 2003-07-22 | Способ непрерывного разделения c4-фракции |
Country Status (15)
Country | Link |
---|---|
US (1) | US7462277B2 (de) |
EP (1) | EP1527036B1 (de) |
JP (1) | JP4575158B2 (de) |
KR (1) | KR100972263B1 (de) |
CN (1) | CN100368354C (de) |
AT (1) | ATE390396T1 (de) |
AU (1) | AU2003250133B2 (de) |
BR (1) | BR0312830B1 (de) |
CA (1) | CA2493079C (de) |
DE (2) | DE10233620A1 (de) |
ES (1) | ES2300621T3 (de) |
MX (1) | MXPA05000491A (de) |
PL (1) | PL208017B1 (de) |
RU (1) | RU2319684C9 (de) |
WO (1) | WO2004011406A1 (de) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2525306C2 (ru) * | 2008-09-17 | 2014-08-10 | Басф Се | Устройства и способ непрерывного дистилляционного разделения смеси, содекржащей один или несколько алканоламинов |
RU2629845C2 (ru) * | 2012-07-25 | 2017-09-04 | Александр Филиппович Кардаш | Способ подготовки углеводородного газа к транспорту |
RU2694032C2 (ru) * | 2014-07-08 | 2019-07-08 | Басф Се | Колонна с разделительными внутренними элементами для разделения смеси углеводородов и/или производных углеводородов путем экстракционной дистилляции с селективным растворителем |
RU2727628C2 (ru) * | 2016-02-05 | 2020-07-22 | Басф Се | Способ разделения веществ с помощью экстрактивной перегонки |
Families Citing this family (41)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10258160A1 (de) * | 2002-12-12 | 2004-06-24 | Basf Ag | Verfahren und Vorrichtung zur Extraktivdestillation |
DE10333756A1 (de) * | 2003-07-24 | 2005-02-17 | Basf Ag | Verfahren zur Auftrennung eines Roh-C4-Schnittes |
US7528290B2 (en) * | 2006-12-28 | 2009-05-05 | Uop Llc | Apparatuses and methods for separating butene-1 from a mixed C4 feed |
CN101050159B (zh) * | 2007-05-17 | 2010-06-23 | 新疆独山子天利高新技术股份有限公司 | 分离丁烷与丁烯的方法及其专用装置 |
KR101127160B1 (ko) * | 2008-10-17 | 2012-03-20 | 금호석유화학 주식회사 | 분리벽형 칼럼을 이용한 공비 혼합물의 분리 방법 |
US8999117B2 (en) * | 2009-03-04 | 2015-04-07 | Uop Llc | Process and system for heating or cooling streams for a divided distillation column |
US8246816B2 (en) * | 2009-03-04 | 2012-08-21 | Uop Llc | Zone or system for providing one or more streams |
CN102336625A (zh) * | 2010-07-28 | 2012-02-01 | 中国石油化工股份有限公司 | 以nmp混合溶剂抽提丁二烯 |
JP5933600B2 (ja) * | 2011-03-03 | 2016-06-15 | ビーエーエスエフ ソシエタス・ヨーロピアBasf Se | ブテンおよび/またはブタジエンを含む物質流を後処理する方法 |
RU2474203C1 (ru) * | 2011-09-21 | 2013-02-10 | Олег Иванович Квасенков | Способ изготовления консервов "треска жареная с грибами" |
KR101372617B1 (ko) * | 2011-11-11 | 2014-03-11 | 주식회사 엘지화학 | 트리할로실란의 정제 장치 |
EP2778132A4 (de) * | 2011-11-11 | 2015-08-26 | Lg Chemical Ltd | Vorrichtung zur veredelung von trihalosilan |
JP5909805B2 (ja) | 2011-11-11 | 2016-04-27 | エルジー・ケム・リミテッド | トリハロシランの精製装置及び精製方法 |
CN102633585A (zh) * | 2012-02-03 | 2012-08-15 | 南京迈森科技发展有限公司 | 一种高纯度丙烷、异丁烷与正丁烷的制备方法 |
WO2014053431A2 (de) | 2012-10-01 | 2014-04-10 | Basf Se | Verfahren zur auftrennung eines gemisches von kohlenwasserstoffen durch extraktivdestillation |
BR112015016172A2 (pt) * | 2013-01-16 | 2017-07-11 | Lg Chemical Ltd | dispositivo para preparar alcanol |
CN104030876B (zh) * | 2013-03-04 | 2016-06-15 | 中国石化工程建设有限公司 | 一种萃取精馏和加氢组合工艺制备异丁烷的系统及方法 |
SG11201507528YA (en) * | 2013-03-18 | 2015-10-29 | Jsr Corp | Production method of 1,3-butadiene |
KR101583146B1 (ko) * | 2013-07-18 | 2016-01-07 | 주식회사 엘지화학 | 분리벽형 증류탑 |
WO2015032804A1 (de) * | 2013-09-05 | 2015-03-12 | Linde Aktiengesellschaft | Verfahren zur erzeugung von kohlenwasserstoffprodukten |
TWI717316B (zh) * | 2014-01-24 | 2021-02-01 | 美商Gtc科技美國有限責任公司 | 用來執行吸收/蒸餾之分離系統 |
US20160083660A1 (en) * | 2014-09-24 | 2016-03-24 | Uop Llc | Fcc process with an integrated secondary reactor for increased light olefin yields |
CN105749575B (zh) * | 2014-12-17 | 2017-12-19 | 新特能源股份有限公司 | 多晶硅生产中的尾气吸收液和冷凝液回收的分隔壁精馏塔、方法、处理系统 |
US10717937B2 (en) | 2015-09-25 | 2020-07-21 | Haldor Topsøe A/S | Process for LPG recovery |
EP3390330B1 (de) * | 2015-12-18 | 2023-07-19 | SABIC Global Technologies B.V. | Verfahren zur herstellung von 1,3-butadien |
JP6888612B2 (ja) * | 2016-03-31 | 2021-06-16 | 日本ゼオン株式会社 | 1,3−ブタジエンの製造方法および製造装置 |
US10343959B2 (en) * | 2016-07-28 | 2019-07-09 | Lyondell Chemical Technology, L.P. | Paraffin removal from C4 containing streams |
CN110198923B (zh) * | 2017-01-25 | 2022-07-22 | 巴斯夫欧洲公司 | 获得纯1,3-丁二烯的方法 |
KR102358406B1 (ko) * | 2017-07-31 | 2022-02-03 | 주식회사 엘지화학 | 라피네이트-2 의 정제 방법 |
CN109593022B (zh) * | 2017-09-30 | 2021-11-02 | 中国石油天然气股份有限公司 | 用于丁二烯抽提的复合萃取剂及其应用 |
KR102387476B1 (ko) * | 2017-11-17 | 2022-04-14 | 주식회사 엘지화학 | 라피네이트-2 의 정제 방법 |
CN108033867A (zh) * | 2017-12-30 | 2018-05-15 | 天津斯瑞吉高新科技研究院有限公司 | 大规模丁烯回收和纯化的简易装置及回收纯化方法 |
CN112135809A (zh) * | 2018-05-18 | 2020-12-25 | 沙特基础工业全球技术有限公司 | 利用水合单元生产燃料添加剂的方法 |
US11207611B1 (en) | 2018-07-03 | 2021-12-28 | Burns & Mcdonnell Engineering Company, Inc. | Process for separating hydrocarbons in a liquid feed utilizing an externally heated reboiler connected to a divided wall column as the primary source of heat energy |
US11952333B2 (en) | 2019-09-13 | 2024-04-09 | Sabic Global Technologies B.V. | Integrated systems and methods for producing 1,3-butadiene via extractive distillation, distillation, and/or selective hydrogenation |
CN114479935B (zh) * | 2020-10-23 | 2023-02-28 | 中国石油化工股份有限公司 | 混合c4物流的加氢装置和加氢方法 |
CN114478161A (zh) * | 2020-10-23 | 2022-05-13 | 中国石油化工股份有限公司 | 混合c4物流选择加氢的装置和方法 |
CN114471375B (zh) * | 2020-10-23 | 2023-02-24 | 中国石油化工股份有限公司 | 混合c4物流全加氢的装置和方法 |
US11236277B1 (en) * | 2020-11-18 | 2022-02-01 | Kellogg Brown & Root Llc | Dividing wall column in a fluid catalytic cracking gas plant for naphtha absorption, stripping, and stabilization service |
EP4108306A1 (de) | 2021-06-25 | 2022-12-28 | Evonik Operations GmbH | Extraktionsdestillationskolonnensystem und dessen einsatz bei der trennung von butenen aus c4-kohlenwasserstoffströmen |
CN114917605A (zh) * | 2022-05-25 | 2022-08-19 | 河北新欣园能源股份有限公司 | 一种节能式多联产c4精馏系统 |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0667329A1 (de) * | 1994-02-11 | 1995-08-16 | ENICHEM S.p.A. | Integriertes Verfahren zur gleichzeitigen Herstellung von Alkyl-Tert-Butylethern und 1-Buten |
FR2757506B1 (fr) * | 1996-12-23 | 1999-02-19 | Inst Francais Du Petrole | Procede de production d'isobutene de haute purete combinant une distillation reactive d'hydroisomerisation et une isomerisation squelettale |
DE19818810A1 (de) * | 1998-04-27 | 1999-10-28 | Basf Ag | Verfahren zum Trennen eines C4-Kohlenwasserstoffgemisches |
DE19849651C2 (de) * | 1998-10-29 | 2003-01-16 | Krupp Uhde Gmbh | Rektifizierkolonne für die Extraktivdestillation von eng- oder azeotrop siedenden Gemischen |
DE10022465A1 (de) * | 2000-05-09 | 2001-11-15 | Basf Ag | Verfahren und Vorrichtung zur Aufarbeitung eines C4-Schnitts aus der Fraktionierung von Erdöl |
IT1319642B1 (it) * | 2000-11-09 | 2003-10-23 | Snam Progetti | Procedimento per la produzione di idrocarburi altoottanici a partireda miscele n-butano/isobutano quali i butani da campo. |
DE10105660A1 (de) * | 2001-02-08 | 2002-08-14 | Basf Ag | Verfahren zur Gewinnung von Roh-1,3-Butadien durch Extraktivdestillation aus einem C4-Schnitt |
DE10219375A1 (de) | 2002-04-30 | 2003-11-13 | Basf Ag | Kontinuierliches Verfahren zur Gewinnung von Butenen aus einem C4-Schnitt |
-
2002
- 2002-07-24 DE DE10233620A patent/DE10233620A1/de not_active Withdrawn
-
2003
- 2003-07-22 AU AU2003250133A patent/AU2003250133B2/en not_active Ceased
- 2003-07-22 RU RU2005105045/04A patent/RU2319684C9/ru active
- 2003-07-22 AT AT03771068T patent/ATE390396T1/de active
- 2003-07-22 ES ES03771068T patent/ES2300621T3/es not_active Expired - Lifetime
- 2003-07-22 CA CA2493079A patent/CA2493079C/en not_active Expired - Fee Related
- 2003-07-22 WO PCT/EP2003/007991 patent/WO2004011406A1/de active IP Right Grant
- 2003-07-22 DE DE50309478T patent/DE50309478D1/de not_active Expired - Lifetime
- 2003-07-22 JP JP2004523761A patent/JP4575158B2/ja not_active Expired - Lifetime
- 2003-07-22 CN CNB038176440A patent/CN100368354C/zh not_active Expired - Lifetime
- 2003-07-22 EP EP03771068A patent/EP1527036B1/de not_active Expired - Lifetime
- 2003-07-22 BR BRPI0312830-0B1A patent/BR0312830B1/pt active IP Right Grant
- 2003-07-22 PL PL375377A patent/PL208017B1/pl not_active IP Right Cessation
- 2003-07-22 MX MXPA05000491A patent/MXPA05000491A/es active IP Right Grant
- 2003-07-22 KR KR1020057001150A patent/KR100972263B1/ko active IP Right Grant
- 2003-07-22 US US10/521,364 patent/US7462277B2/en active Active
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2525306C2 (ru) * | 2008-09-17 | 2014-08-10 | Басф Се | Устройства и способ непрерывного дистилляционного разделения смеси, содекржащей один или несколько алканоламинов |
RU2525306C9 (ru) * | 2008-09-17 | 2014-11-20 | Басф Се | Устройства и способ непрерывного дистилляционного разделения смеси, содержащей один или несколько алканоламинов |
RU2629845C2 (ru) * | 2012-07-25 | 2017-09-04 | Александр Филиппович Кардаш | Способ подготовки углеводородного газа к транспорту |
RU2694032C2 (ru) * | 2014-07-08 | 2019-07-08 | Басф Се | Колонна с разделительными внутренними элементами для разделения смеси углеводородов и/или производных углеводородов путем экстракционной дистилляции с селективным растворителем |
RU2727628C2 (ru) * | 2016-02-05 | 2020-07-22 | Басф Се | Способ разделения веществ с помощью экстрактивной перегонки |
Also Published As
Publication number | Publication date |
---|---|
CN1671638A (zh) | 2005-09-21 |
PL375377A1 (en) | 2005-11-28 |
PL208017B1 (pl) | 2011-03-31 |
ATE390396T1 (de) | 2008-04-15 |
WO2004011406A1 (de) | 2004-02-05 |
AU2003250133B2 (en) | 2009-12-03 |
RU2319684C2 (ru) | 2008-03-20 |
DE10233620A1 (de) | 2004-02-12 |
JP4575158B2 (ja) | 2010-11-04 |
DE50309478D1 (de) | 2008-05-08 |
JP2006502122A (ja) | 2006-01-19 |
US20060021911A1 (en) | 2006-02-02 |
CA2493079A1 (en) | 2004-02-05 |
US7462277B2 (en) | 2008-12-09 |
EP1527036B1 (de) | 2008-03-26 |
ES2300621T3 (es) | 2008-06-16 |
EP1527036A1 (de) | 2005-05-04 |
RU2005105045A (ru) | 2005-07-20 |
BR0312830B1 (pt) | 2013-07-09 |
CA2493079C (en) | 2012-03-20 |
AU2003250133A1 (en) | 2004-02-16 |
MXPA05000491A (es) | 2005-03-23 |
BR0312830A (pt) | 2005-04-26 |
CN100368354C (zh) | 2008-02-13 |
KR100972263B1 (ko) | 2010-07-23 |
KR20050025644A (ko) | 2005-03-14 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
RU2319684C9 (ru) | Способ непрерывного разделения c4-фракции | |
RU2279421C2 (ru) | Способ получения сырого 1,3-бутадиена экстрактивной дистилляцией c4-фракции и установка для его осуществления | |
RU2330005C2 (ru) | Способ получения неочищенного 1,3-бутадиена | |
US7432411B2 (en) | Continuous method for obtaining butenes from a C4 fraction | |
KR101084866B1 (ko) | 조 c4 분획의 분리방법 | |
RU2310640C2 (ru) | Способ выделения сырого 1,3-бутадиена из c4-фракции | |
RU2318791C2 (ru) | Способ переработки сырого 1,3-бутадиена | |
KR100741214B1 (ko) | C4 분획을 처리하기 위한 방법 및 장치 | |
US8766029B2 (en) | Process for providing a vaporous purified crude C4 cut as a feed steam for an extractive distillation with a selective solvent | |
Adrian et al. | Continuous method for separating a C 4 cut | |
Heida et al. | Method for the separation of a crude C 4 cut |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
TH4A | Reissue of patent specification | ||
PD4A | Correction of name of patent owner | ||
QB4A | Licence on use of patent |
Free format text: LICENCE Effective date: 20140711 |